Linde has designed an oxygen generator in many respects similar to the Claude generator, but working without the expan sion engine, which is really only effective in connection with large plants.
Liquid oxygen is used as an explosive by absorbing it by char coal, or other combustible material, contained in a paper cart ridge, and exploding the charge by fuse and detonator. Charcoal is used which absorbs upwards of three times its weight of liquid oxygen, so as to ensure complete combustion, according to the The heat evolved in exploding black powder and blasting gelatine is approximately 700 and 1,65o KC. respectively, and though the heat liberated is not a direct measure of the effectiveness of an explosive, it serves as an indication of it. Liquid air explosives have the particular advantage that they give rise to no noxious fumes, and misfires are not a source of danger.
liquid can be drawn off and submitted to further fractional evapo ration. Neon and helium are also produced on a manufacturing scale by condensation and rectification of the most volatile frac tion of the liquid air.
As an example of the application of low temperatures to the separation of gases by liquefaction and fractional distillation we may take the investigations of Ramsay and Travers on the inac tive constituents of the atmosphere. By evaporation of liquid air a small residue of liquid was obtained which was found to con sist mainly of oxygen. On removal of oxygen a residue was ob tained which on spectroscopic examination was found to consist mainly of argon ; but which evidently contained some previously unknown gas. The density of this residue was slightly greater than that of argon. Larger quantities of the residue were obtained and the gas was then treated in the following manner :—It was intro duced into the reservoir A of the apparatus shown in fig. 25, and this communicated through a stopcock with the bulb C which was immersed in liquid air contained in a vacuum vessel, and through the stopcock D with a mercury pump. The bulb C was exhausted, the stopcock D was closed, and the gas from A was allowed to flow into C, in which it was condensed, either by increasing the pres sure in A, by raising the mercury reservoir connected with it, or by lowering the temperature of the liquid air by connecting the outlet from the vacuum vessel with an exhaust pump. This pro cedure was necessary since the gas consisted mainly of argon which boils at —185.7° C., while the temperature of liquid air consisting mainly of oxygen was about —183° C. When the whole of the gas was condensed it was allowed to evaporate, the gas passing back into A in six successive fractions; i.e., when a small quantity of gas had collected in A the stopcock was closed and this gas was transferred to a storage tube. Further quantities of gas were collected in the same manner, and finally the stopcock C was closed, the stopcock D was opened, the liquid was removed and the residue remaining in B passed into the mercury pump, which was arranged so that this quantity of gas could also be col lected. Numbering the fractions obtained two to seven, fraction two, the fraction collected first, contained the most volatile gas, and fraction seven the least volatile gas. Fraction two was dis carded; fraction three was then introduced into A and condensed in the bulb C. About two-thirds of it was then allowed to evapo rate back into A and the gas was transferred to a storage tube as fraction eight. Fraction four was then condensed with the residue in C, and again par tially evaporated, the most vola tile portion forming fraction nine. The same operation was re peated with fractions five, six and seven, and new fractions ten, i i and 12 were collected through A, a last fraction, 13, being taken into the pump and collected as before.